EP0051463A2 - Sedimentieren flüssiger Dispersionen - Google Patents
Sedimentieren flüssiger Dispersionen Download PDFInfo
- Publication number
- EP0051463A2 EP0051463A2 EP81305155A EP81305155A EP0051463A2 EP 0051463 A2 EP0051463 A2 EP 0051463A2 EP 81305155 A EP81305155 A EP 81305155A EP 81305155 A EP81305155 A EP 81305155A EP 0051463 A2 EP0051463 A2 EP 0051463A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- dispersion
- electrodes
- pair
- electrostatic field
- flow path
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/06—Separation of liquids from each other by electricity
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G33/00—Dewatering or demulsification of hydrocarbon oils
- C10G33/02—Dewatering or demulsification of hydrocarbon oils with electrical or magnetic means
Definitions
- the present invention relates to methods and apparatus for settling liquid dispersions or emulsions and particularly separating two immiscible or partially miscible liquids.
- pulsed d.c. fields has also been proposed, the frequency of such fields being of the order of lO kilohertz (kHz).
- apparatus for aiding the separation of the components of a liquid dispersion, the apparatus comprising means for passing said dispersion along a flow path, and at least one pair of electrodes for applying a unidirectional, varying electrostatic field across at least a portion of the flow path, at least one of the or each pair of electrodes being arranged so that, in use, it is separated from the dispersion by a layer of insulating material.
- the present invention also provides a method for aiding the separation of the components of a liquid dispersion, the method comprising passing said dispersion along a flow path and applying by means of at least one pair of electrodes a unidirectional, varying electrostatic field across at least a portion of the flow path, at least one of the or each pair of electrodes being arranged so that it is separated from the dispersion by a layer of insulating material.
- the invention involves the combination of three factors to give an unexpected and highly efficient method of liquid phase separation.
- the factors are firstly that the electric field applied across the dispersion must be unidirectional. Secondly, this field must be fluctuating, for instance, regular or irregular variation of the voltage level. Preferably the variation is periodic and more preferably pulsed between zero voltage and some appropriate high voltage at a predetermined constant frequency. Finally, the high voltage electrode or both electrodes must be separated from the dispersion and thereby prohibited from contacting the dispersion by a layer of insulating material, for example, perspex or air.
- the liquid dispersion is a dispersion of one or more electrically conducting liquids in one or more less electrically conducting liquids. More preferably the liquid dispersion is a dispersion of an electrically conducting liquid in an electrically insulating liquid.
- the apparatus is particularly well-suited to the treatment of dispersions where the volume of conducting liquid as a percentage of the total volume of dispersion is high, for example, 50%.
- the degree of liquid phase separation within the apparatus is controlled by the frequency and magnitude of said variation of the electrostatic field.
- the frequency at which the electric field is varied can have a specific value for which phase separation is optimum.
- This optimum frequency depends on the thickness and electrical properties of the electrode insulation and on the properties of the dispersion that is being treated.
- typically a preferred frequency of variation of the electrostatic field is between 30 Hz and 1 Hz. More preferably it is between 20 Hz and 1.5 Hz and most preferably it is between 15 Hz and 2 Hz. It should be appreciated, however, that the optimum frequency may well lie outside the above preferred ranges, and in any case good results may be obtained at frequencies other than the optimum frequency.
- phase separation performance can be expected to be very sensitive to the frequency of the electric field fluctuation. For any particular operating voltage there is an optimum frequency, where the operating voltage is above or below 300 volts per cm.
- the higher the voltage the better the separation of the phases but it is preferred to use the lower voltages having regard to factors such as safety, capital costs and operating costs. Having regard to these factors the preferred electric field strength across the flow path is below 1100 volts per cm. More preferably it is below 500 volts per cm and most preferably it is below 100 volts per cm.
- apparatus in accordance with the present invention effects separation of the components of a dispersion at much lower frequencies than had previously been considered. Furthermore separation at much lower frequencies has led to the appreciation that dispersions can be efficiently separated into their component liquids at field strengths far below those previously employed. Furthermore the equipment is safer to operate because of the avoidance of very high voltages in an environment in which flammable organic materials are likely to be present.
- This invention also provides a process for aiding the separation of the components of a liquid dispersion, the process comprising passing the dispersion along a flow path, and applying across at least a portion of the flow path a varying electrostatic field.
- Apparatus and processes in accordance with the present invention may be used in many situations where a mixture of two or more liquids is to be separated into its component liquids. Examples are as follows:
- Apparatus in accordance with the present invention may be used alone or in conjunction with a settling tank depending upon the degree of separation effected by the application of the electrostatic field.
- a dispersion may be passed along a duct between a pair, or a plurality of pairs, of electrodes and then fed from the duct into a settling tank which may be provided with one or more baffles positioned close to the point of entry of the liquid mixture into the tank in order to reduce the turbulence in the tank.
- Each separated liquid phase can be drawn off at an appropriate rate in order to keep the total volume of the liquid in the tank substantially constant.
- apparatus in accordance with the present invention comprises mixer container 1 into which the two immiscible liquids are fed.
- the liquids are intimately mixed by agitator 2 driven at high speed by mixer motor 3.
- the resultant dispersion is then fed through a tube 4 into an electrostatic coalescer 5.
- Coalescer 5 includes a shallow perspex "duct" 5a / which is approximately square in plan and which is located on a support 6 so as to be inclined gently upwards in the direction of the liquid flow.
- Metal plates (not shown) are located on the exterior surface of the top and the interior surface of the base of the duct 5a, the upper metal plate being charged and the lower metal plate being earthed.
- Drain valve 8 This may be used to drain the contents of the coalescer at shut down and could be used to remove coalesced aqueous or conducting phase in order to keep the surface of the aqueous phase at a constant level in the duct.
- exit pipe 9 leading to a settler tank 10.
- Tank 10 has located therein vertical baffles lla and llb which define portions 11c and 11d of the tank. Within portion llc the turbulence of the liquid being fed into the tank through tube 9 is dissipated. In portion 11d there is, during operation of the apparatus, set up a steady state position in which dispersion 12 lies between organic phase 13 and aqueous phase 14. The depth of dispersion 12 may be used as a measure of the effectiveness of the apparatus in achieving separation of the dispersion into its component phases. The smaller the depth of the dispersion the more effective is the electrostatic coalescer 5.
- a further baffle lie allows organic phase 13 to accumulate in portion llf of tank 10 and to be led off therefrom through pipe 16.
- Aqueous phase may be led off from a central portion of the tank between baffles llb and lie through pipe 15.
- the electrical circuit used to charge up plate 5 of the electrostatic coalescer is shown in Figure 2.
- a variable supply from an EHT generator of up to 15 kilovolts is alternately switched on and off by means of a shunt stabilised triode 20 as used in colour television EHT valves.
- the grid of the triode is connected to a signal generator 23 with a range of frequencies of from 0.5 to 60 hertz, the generator being in parallel with a 1 M ⁇ resistor 24.
- the cathode 26 of the valve is connected to earth and is heated by a 7.3 volt a.c. heater 27.
- the anode 22 of the valve is connected in series with a 100 M ⁇ resistor 19 and thence to the EHT input.
- the voltage on the anode is fed via line 21 to the top plate of the electrostatic coalescer 5.
- the supply to the triode heater 27 can be derived by any suitable means.
- the heater supply is derived from an a.c. main supply of the standard 240 V, 50 Hz.
- terminal 34 is the live terminal
- terminal 35 is neutral
- 36 is earth.
- the lead from the live terminal 36 is taken to a first terminal of the primary winding 29 of a 7.3 V a.c. 0.3A transformer, via a main ON/ OFF switch 33 and a 1A fuse 32 in series with the live supply lead.
- the second terminal of the primary winding 29 of the transformer is led via a.second pole of the previously mentioned ON/OFF switch 33 to the neutral terminal 35.
- Comprising the remainder of the transformer assembly is an iron core and secondary winding 28.
- a first terminal of secondary winding 28 is connected to earth rail 36.
- the second terminal of secondary winding 28 is connected to a first terminal of triode heater element 27, the second terminal of heater element 27 being connected to earth rail 36.
- connection of the mains a.c. supply to primary winding 29 induces an a.c. voltage across secondary winding 28 of, in this case, 7.3 V. This causes an alternating current to flow through heater element 27, thus generating heat energy which may be transmitted to electrons on cathode 26.
- the above-described control circuit for the electrostatic coalescer operates to connect the top plate electrode alternately to ground, via the triode valve, and to the supply from the EHT generator. The result is that a pulsed d.c. unidirectional current is delivered to this electrode, the pulses being of substantially square wave form (see Figure 3).
- Table 1 illustrates the results obtainable using the above-described apparatus on the second of the dispersions described above.
- the peak electric field values given in Table 1 are those obtaining inside duct 5a as measured by the probes 7.
- the reduction in dispersion band depth is the ratio, expressed as a percentage, of the depth of dispersion 12 in tank 10 when the electrostatic field is applied across duct 5a to the depth when the field is not so applied.
- Apparatus in accordance with the present invention may or may not include a settling tank of a size appropriate for the process in which the apparatus is to be used. Having regard to the extent of settling achieved by the application of the electrostatic field, such a settling tank where it is included can be of substantially smaller capacity than those which would have been necessary without the use of the electrostatic field to effect precoalescing of the dispersed phase.
- Apparatus in accordance with the present invention may, instead of including its own settling tank, be added to existing equipment including settling tanks.
- the addition of such apparatus will enable the settling stage of the overall process to be effected very much more rapidly for a given throughput, and in practice the throughput of the overall process can be greatly increased.
- Apparatus in accordance with the present invention when added to existing equipment including settling tanks may take a form where one electrode is suspended above said equipment, insulated from the liquid contents by air or an inert gaseous atmosphere.
- the fluctuating unidirectional electrostatic field can be applied between suitably insulated wires immersed in the flow path of the dispersion, the electrical connections and spatial arrangement of said wires being such that they form a plurality of pairs of electrodes.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT81305155T ATE29673T1 (de) | 1980-11-01 | 1981-10-30 | Sedimentieren fluessiger dispersionen. |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB8035196 | 1980-11-01 | ||
GB8035196 | 1980-11-01 | ||
GB8123653 | 1981-08-03 | ||
GB8123653 | 1981-08-03 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0051463A2 true EP0051463A2 (de) | 1982-05-12 |
EP0051463A3 EP0051463A3 (en) | 1983-01-26 |
EP0051463B1 EP0051463B1 (de) | 1987-09-16 |
Family
ID=26277394
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP81305155A Expired EP0051463B1 (de) | 1980-11-01 | 1981-10-30 | Sedimentieren flüssiger Dispersionen |
Country Status (4)
Country | Link |
---|---|
US (1) | US4601834A (de) |
EP (1) | EP0051463B1 (de) |
CA (1) | CA1176205A (de) |
DE (1) | DE3176445D1 (de) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2143157A (en) * | 1983-07-15 | 1985-02-06 | Electricity Council | Electrostatically removing water from oil |
EP0148380A2 (de) * | 1983-12-09 | 1985-07-17 | Heinz Doevenspeck | Elektroimpulsverfahren und Vorrichtung zur Behandlung von Stoffen |
GB2171031A (en) * | 1985-02-20 | 1986-08-20 | Univ Bradford | Electrostatic separation of liquid dispersions |
DE3709456A1 (de) * | 1987-03-23 | 1988-10-06 | Univ Hannover | Verfahren und vorrichtung zur spaltung von fluessigmembranemulsionen aus metallextraktionsprozessen |
AT390013B (de) * | 1988-06-03 | 1990-03-12 | Rolf Dipl Ing Dr Techn Marr | Verfahren und vorrichtung zur spaltung von emulsionen |
NL1003591C2 (nl) * | 1996-07-15 | 1998-01-21 | Dsm Nv | Electrostatische coalescentie. |
US6428669B2 (en) | 1999-12-27 | 2002-08-06 | Abb Research Ltd | Method for separating the constituents of a dispersion |
WO2002089947A1 (en) * | 2001-05-04 | 2002-11-14 | Abb Research Ltd. | A device for coalescing a fluid |
WO2007017230A2 (de) | 2005-08-08 | 2007-02-15 | MAX-PLANCK-Gesellschaft zur Förderung der Wissenschaften e.V. | Bildung einer emulsion in einem fluidischen mikrosystem |
Families Citing this family (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3635450A1 (de) * | 1986-10-18 | 1988-04-21 | Metallgesellschaft Ag | Verfahren zur selektiven gewinnung von germanium und/oder arsen aus waessrigen loesungen |
US4865747A (en) * | 1988-01-27 | 1989-09-12 | Aqua-D Corp. | Electromagnetic fluid treating device and method |
US4960524A (en) * | 1988-04-18 | 1990-10-02 | Inculet Ion I | Method for soil consolidation |
US4963268A (en) * | 1988-04-20 | 1990-10-16 | Aqua Dynamics Group Corp. | Method and system for variable frequency electromagnetic water treatment |
US4865748A (en) * | 1988-04-20 | 1989-09-12 | Aqua-D Corp. | Method and system for variable frequency electromagnetic water treatment |
US5113751A (en) * | 1990-05-31 | 1992-05-19 | Aqua Dynamics Group Corp. | Beverage brewing system |
GB9206335D0 (en) * | 1992-03-24 | 1992-05-06 | Univ Bradford | Resolution of emulsions |
US5575896A (en) * | 1994-04-06 | 1996-11-19 | National Tank Company | Method and apparatus for oil/water separation using a dual electrode centrifugal coalescer |
US5565078A (en) * | 1994-04-06 | 1996-10-15 | National Tank Company | Apparatus for augmenting the coalescence of water in a water-in-oil emulsion |
US5861087A (en) * | 1996-11-12 | 1999-01-19 | National Tank Company | Apparatus for augmenting the coalescence of a component of an oil/water mixture |
NO312404B1 (no) * | 2000-05-05 | 2002-05-06 | Aibel As | In-line elektrostatiske koalescer med doble heliske elektroder |
US20030089650A1 (en) * | 2001-10-02 | 2003-05-15 | Renfro William Leonard | Automatic, renewable separation & filtration system for liquids |
NO316837B1 (no) * | 2001-10-17 | 2004-05-24 | Norsk Hydro As | Anordning for separasjon av fluider |
US7351320B2 (en) * | 2002-08-07 | 2008-04-01 | National Tank Company | Multiple frequency electrostatic coalescence |
US7758738B2 (en) | 2002-08-07 | 2010-07-20 | National Tank Company | Separating multiple components of a stream |
US6860979B2 (en) * | 2002-08-07 | 2005-03-01 | National Tank Company | Dual frequency electrostatic coalescence |
NO318190B1 (no) * | 2003-07-09 | 2005-02-14 | Norsk Hydro As | Rorseparator |
FR2871070B1 (fr) * | 2004-06-02 | 2007-02-16 | Commissariat Energie Atomique | Microdispositif et procede de separation d'emulsion |
US8591714B2 (en) | 2007-04-17 | 2013-11-26 | National Tank Company | High velocity electrostatic coalescing oil/water separator |
DE102011008183A1 (de) * | 2011-01-10 | 2012-07-12 | New Environmental Technology Gmbh | Kontinuierliche Aufbereitung eines Kühlschmierstoffs |
US9095790B2 (en) | 2012-06-08 | 2015-08-04 | Cameron International Corporation | High velocity electrostatic coalescing oil/water separator |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB191313564A (en) * | 1913-06-12 | 1914-06-11 | Cyril Yeoman | Improvements in Life Saving Attachments for Wheeled Vehicles. |
DE733842C (de) * | 1935-09-05 | 1943-04-02 | Erdoelproduktions Ges M B H | Vorrichtung zur kontinuierlichen Abscheidung von Wasser und Feststoffen aus Erdoelemulsionen |
US2364118A (en) * | 1939-04-05 | 1944-12-05 | Petrolite Corp | Method and apparatus for electrically treating fluids |
BE674733A (de) * | 1964-09-10 | 1966-07-04 | ||
DE2743417A1 (de) * | 1977-09-27 | 1979-04-05 | Maloney Crawford Corp | Vorrichtung zur trennbehandlung von emulsionen |
US4226690A (en) * | 1979-05-29 | 1980-10-07 | Petrolite Corporation | Process for dehydration and demineralization of diluted bitumen |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB191313465A (en) * | 1913-06-10 | 1914-06-10 | British Thomson Houston Co Ltd | Improvements in and relating to the Separation of Liquid Suspensions. |
US4283290A (en) * | 1977-07-06 | 1981-08-11 | Davy International (Oil & Chemicals) Ltd. | Purification utilizing liquid membrane with electrostatic coalescence |
GB1582040A (en) * | 1977-09-06 | 1980-12-31 | Maloney Crawford Corp | Dual field electric treater |
US4290882A (en) * | 1978-12-21 | 1981-09-22 | Davy Powergas Inc. | Electrostatic separation of impurities phase from liquid-liquid extraction |
-
1981
- 1981-10-30 DE DE8181305155T patent/DE3176445D1/de not_active Expired
- 1981-10-30 EP EP81305155A patent/EP0051463B1/de not_active Expired
- 1981-11-02 CA CA000389182A patent/CA1176205A/en not_active Expired
-
1983
- 1983-10-04 US US06/538,940 patent/US4601834A/en not_active Expired - Lifetime
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB191313564A (en) * | 1913-06-12 | 1914-06-11 | Cyril Yeoman | Improvements in Life Saving Attachments for Wheeled Vehicles. |
DE733842C (de) * | 1935-09-05 | 1943-04-02 | Erdoelproduktions Ges M B H | Vorrichtung zur kontinuierlichen Abscheidung von Wasser und Feststoffen aus Erdoelemulsionen |
US2364118A (en) * | 1939-04-05 | 1944-12-05 | Petrolite Corp | Method and apparatus for electrically treating fluids |
BE674733A (de) * | 1964-09-10 | 1966-07-04 | ||
DE2743417A1 (de) * | 1977-09-27 | 1979-04-05 | Maloney Crawford Corp | Vorrichtung zur trennbehandlung von emulsionen |
US4226690A (en) * | 1979-05-29 | 1980-10-07 | Petrolite Corporation | Process for dehydration and demineralization of diluted bitumen |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2143157A (en) * | 1983-07-15 | 1985-02-06 | Electricity Council | Electrostatically removing water from oil |
EP0148380A2 (de) * | 1983-12-09 | 1985-07-17 | Heinz Doevenspeck | Elektroimpulsverfahren und Vorrichtung zur Behandlung von Stoffen |
EP0148380A3 (en) * | 1983-12-09 | 1986-03-05 | Heinz Doevenspeck | Electroimpulse process, and device for treating material with it |
GB2171031A (en) * | 1985-02-20 | 1986-08-20 | Univ Bradford | Electrostatic separation of liquid dispersions |
GB2171031B (en) * | 1985-02-20 | 1989-07-05 | Univ Bradford | Settling of liquid dispersions |
DE3709456A1 (de) * | 1987-03-23 | 1988-10-06 | Univ Hannover | Verfahren und vorrichtung zur spaltung von fluessigmembranemulsionen aus metallextraktionsprozessen |
AT390013B (de) * | 1988-06-03 | 1990-03-12 | Rolf Dipl Ing Dr Techn Marr | Verfahren und vorrichtung zur spaltung von emulsionen |
NL1003591C2 (nl) * | 1996-07-15 | 1998-01-21 | Dsm Nv | Electrostatische coalescentie. |
WO1998002225A1 (en) * | 1996-07-15 | 1998-01-22 | Dsm N.V. | Electrostatic coalescence |
US6428669B2 (en) | 1999-12-27 | 2002-08-06 | Abb Research Ltd | Method for separating the constituents of a dispersion |
WO2002089947A1 (en) * | 2001-05-04 | 2002-11-14 | Abb Research Ltd. | A device for coalescing a fluid |
US7520985B2 (en) | 2001-05-04 | 2009-04-21 | Aibel As | Device for coalescing a fluid |
WO2007017230A2 (de) | 2005-08-08 | 2007-02-15 | MAX-PLANCK-Gesellschaft zur Förderung der Wissenschaften e.V. | Bildung einer emulsion in einem fluidischen mikrosystem |
WO2007017230A3 (de) * | 2005-08-08 | 2007-04-12 | Max Planck Gesellschaft | Bildung einer emulsion in einem fluidischen mikrosystem |
US7943671B2 (en) | 2005-08-08 | 2011-05-17 | Max-Planck-Gesellschaft Zur Foerderung Der Wissenschaften E.V. | Formation of an emulsion in a fluid microsystem |
Also Published As
Publication number | Publication date |
---|---|
DE3176445D1 (en) | 1987-10-22 |
EP0051463A3 (en) | 1983-01-26 |
US4601834A (en) | 1986-07-22 |
CA1176205A (en) | 1984-10-16 |
EP0051463B1 (de) | 1987-09-16 |
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